DP FlowFluid Data Sheetcd Flow Fluid Sheet
User Manual: DP-Flow Fluid Data Sheet
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Catalog 2002 – 2003 This form identifies custom fluids that are not in the Rosemount Fluid Database. Complete this form for the following DP Flowmeters (if applicable): • • • Annubar Flowmeter Series Model 405P Compact Orifice Model 1195 Integral Orifice, ProPlate Flowmeter, Mass ProPlate Flowmeter For technical assistance in filling out this CDS, call your local Rosemount representative. Complete this form to define a custom fluid. The ★ symbol identifies the default value. NOTE This form is not required if using the Rosemount Fluid Database. * = Required Item ★ = Default Customer Information Customer: Contact Name: Customer Phone: Customer Fax: Customer PO: Fluid Properties ❑ Custom Liquid– Complete Table ❑ Liquid ❑ Custom Gas– Complete Table ❑ Gas ❑ Custom Natural Gas– Complete Table ❑ Natural Gas For Rosemount Use Only S.O.: LI CHAMP: DATE: ADMIN: Flow-105 Catalog 2002 – 2003 TABLE 1. Custom Liquid Worksheet * = Required Item ★ = Default Mass Liquid Density and Viscosity Information 1. Fill in the following operating temperatures a) _________________________ min b) _________________________ [1/3 (max - min))] + min c) _________________________ [2/3 (max - min))] + min d) _________________________ max 2. Transfer the values from the above section to the numbered lines below. 3. Check one Density box, then enter the values for each temperature and the standard density. 4. Check one Viscosity box, then enter values for each temperature. (At least one viscosity value is required). Density Viscosity ❑ Density in lbs/CuFt ❑ Viscosity in centipoise ❑ Density in kg/CuM ❑ Viscosity in lbs/ft sec ❑ Viscosity in pascal sec Temperature a) _____________ min Temperature a) _____________ min. b) _____________ [1/3 (max - min))] + min b) _____________ [1/3 (max - min))] + min c) _____________ [2/3 (max - min))] + min c) _____________ [2/3 (max - min))] + min d) _____________ max d) _____________ max Base density: __________________________________________________________ (at base reference conditions specified) Volumetric Liquid Density and Viscosity Information * Density at Flow: _________________________________________________ Units: ❑ lb/ft3 ❑ Kg/m3 ❑ Other: OR Specific Gravity at Flow: ____________________________________________ * Viscosity at Flow: ________________________________________________ Units: ❑ Centipoise Flow-106 ❑ Other: Catalog 2002 – 2003 TABLE 2. Custom Gas Worksheet * = Required Item ★ = Default Mass Gas Compressibility and Viscosity Information 1. Fill in the following operating pressures and operating temperatures Operating Pressures Operating Temperatures a) _____________ min e) _____________ min b) _____________ [1/3 (max - min))] + min f) _____________ [1/2 (max - min))] + min c) _____________ [2/3 (max - min))] + min g) _____________ max d) _____________ max h) _____________ [1/3 (max - min))] + min i) _____________ [2/3 (max - min))] + min 2. 3. 4. 5. Transfer the values from the above section to the numbered lines below Check one Density/Compressibility box, then enter the 12 values for each pressure/temperature range. Check one Viscosity box, then enter values for each temperature. (At least one viscosity value is required). Enter values for molecular weight, isentropic exponent, and standard density (or standard compressibility). Density Viscosity ❑ Density in lbs/CuFt ❑ Viscosity in centipoise ❑ Density in kg/CuM ❑ Viscosity in lbs/ft sec ❑ Compressibility ❑ Viscosity in pascal sec Pressure Temperature Temperature 1) ____________ 5) _____________________________ 5) ________________________________________ 2) ____________ 5) _____________________________ 8) ________________________________________ 3) ____________ 5) _____________________________ 9) ________________________________________ 4) ____________ 5) _____________________________ 7) ________________________________________ 1) ____________ 6) _____________________________ 2) ____________ 6) _____________________________ Molecular Weight: _________________________ 3) ____________ 6) _____________________________ Isentropic Exponent: _______________________ 1.4 ★ 4) ____________ 6) _____________________________ 1) ____________ 7) _____________________________ 2) ____________ 7) _____________________________ 3) ____________ 7) _____________________________ 4) ____________ 7) _____________________________ Standard density/compressibility: __________________________________________________________ Volumetric Gas Compressibility and Viscosity Information * Density at Flow: ______________________________ Units: ❑ lb/ft3 ❑ Kg/m3 ❑ Other: OR M.W. / Specific Gravity at Flow: _________________________________________________ Compressibility at Flow: _____________________________________________________ Compressibility at Base: ____________________________________________________ * Viscosity at Flow: _____________________________ Units: ❑ Centipoise ❑ Other: Isentropic Exponent (K):______ 1.4 ★ Flow-107 Catalog 2002 – 2003 TABLE 3. Natural Gas Worksheet NOTE The minimum requirement for the Volumetric options is highlighted gray on page Flow-108. * = Required Item ★ = Default Compressibility Factor Information Choose desired character4ization method and only enter values for that method. ❑ Detail Characterization Method (AGA8 1992) CH4 N2 CO2 C2H6 C3H8 H2O H2S H2 CO O2 C4H10 C4H10 C5H12 C5H12 C8H18 C7H18 C8H18 C9H2O C10H22 He Ar Methane mole percent Nitrogen mole percent Carbon Dioxide mole percent Ethane mole percent Propane mole percent Water mole percent Hydrogen Sulfide mole percent Hydrogen mole percent Carbon monoxide mole percent Oxygen mole percent i-Butane mole percent n-Butane mole percent i-Pentane mole percent n-Pentane mole percent Hexane mole percent n-Heptane mole percent n-Octane mole percent n-Nonane mole percent n-Decane mole percent Helium mole percent Argon mole percent ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ ❑ Gross Characterization Method, Option Code 1 (AGA8 Gr-Hv-CO2) Specific Gravity at 14.73 psia and 60 °F ________________________________ Volumetric gross heating value at base conditions Carbon Dioxide mole percent Hydrogen mole percent Carbon Monoxide mole percent ________________________________ ________________________________ ________________________________ ________________________________ ❑ Gross Characterization Method, Option Code 2 (AGA8 Gr-CO2-N2) Specific Gravity at 14.73 psia and 60 °F Carbon Dioxide mole percent Nitrogen mole percent Hydrogen mole percent Carbon Monoxide mole percent ________________________________ ________________________________ ________________________________ ________________________________ ________________________________ (1) The summaries of i-Butane and n-Butane cannot exceed 6 percent. (2) The summaries of i-Pentane and n-Pentane cannot exceed 4 percent. Flow-108 Mole Valid Range % % % % % % % % % % % % % % % % % % % % % 0 – 100 percent 0 – 100 percent 0 – 100 percent 0 – 100 percent 0 – 12 percent 0 – Dew point 0 – 100 percent 0 – 100 percent 0 – 3.0 percent 0 – 21 percent 0 – 6 percent(1) 0 – 6 percent(1) 0 – 4 percent(2) 0 – 4 percent 0 – Dew Point 0 – Dew Point 0 – Dew Point 0 – Dew Point 0 – Dew Point 0 – 3.0percent 0 – 1.0 percent Mole Valid Range 0.554 – 0.87 BTU/SCF % % % 477 – 1150 BTU/SCF 0 – 30 percent 0 – 10 percent 0 – 3.0 percent Mole Valid Range % % % % % 0.554 – 0.87 0 – 30 percent 0 – 50 percent 0 – 10 percent 0 – 3.0 percent
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